• 제목/요약/키워드: $H_2S$ removal

검색결과 779건 처리시간 0.031초

철과 망간이 동시에 코팅된 반응성 매질을 이용한 용존 Fe(II) 제거 (Removal of Soluble Fe(II) using Reactive Media Coated with both Fe and Mn)

  • 민상윤;장윤영;양재규
    • 대한환경공학회지
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    • 제33권2호
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    • pp.85-92
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    • 2011
  • 본 연구에서는 산화망간과 산화철이 단독 및 복합 코팅된 반응성매질인 망간코팅사(MCS), 철코팅사(ICS) 그리고 철-망간코팅사(IMCS)를 이용하여 용존 Fe(II)의 산화 및 제거능을 평가하였다. 반응성매질에 $KMnO_4$와 NaOCl를 추가적인 산화제로 이용하였을 때의 Fe(II) 제거능을 반응용액의 pH, 반응시간, Fe(II) 농도변화에 따라 조사하였다. 반응성매질 및 추가적인 산화제 없이 Fe(II) 용액만을 사용한 경우, pH 5 이하에서는 Fe(II)의 느린 산화에 의해 제거율이 낮았으나 이후에는 빠른 산화 및 침전반응에 의해 제거율이 증가하였다. ICS만을 사용하였을 때 ICS 표면에 의한 Fe(II)의 제거는 극히 제한적인 것으로 나타났다. 망간 산화물이 코팅된 IMCS와 MCS를 사용한 경우 낮은 pH에서도 Fe(II)가 산화망간에 의해 산화되었으며 용액으로부터 효과적으로 제거되는 것으로 나타났다. Fe(II)는 IMCS만 단독으로 사용했을 때와 NaOCl을 산화제로 사용했을 때 제거율에서 큰 차이가 나지 않았다. IMCS와 산화제를 이용하여 Fe(II)을 제거할 경우, 용액의 pH가 증가함에 따라 이들의 산화능이 증가하였고 이로써 전체 제거율의 증가를 가져왔다. Fe(II)의 제거에 관한 반응속도 실험결과 유사-1차 반응 보다는 유사-2차 반응식으로 더 잘 표현되었으며 $KMnO_4$를 추가적인 산화제로 이용한 경우 Fe(II)는 14,286 mg/kg hr의 높은 초기 제거율(h)을 보였다. $KMnO_4$ 주입 시 반응시간 10분 안에 제거평형에 도달하였고 NaOCl의 경우는 6시간 후에 거의 제거평형에 도달하는 것으로 나타났다. IMCS에 의한 Fe(II)의 최대 제거량 값을 구하기 위해 pH 4에서 Langmuir 등온식에 적용한 결과 1,088 mg/kg의 제거량을 보였다.

ZnO-Fe2O3 복합금속 산화물을 이용한 고온에서의 황화수소 제거에 관한 연구 (High Temperature Desulfurization over ZnO-Fe2O3 Mixed Metal Oxide Sorbent)

  • 이재복;이영수;류경옥
    • 한국환경보건학회지
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    • 제20권1호
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    • pp.62-67
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    • 1994
  • ZnO-$Fe_2O_3$ 복합금속 산화물 흡착제가 황화수소 제거능이나 황화된 흡착제의 산화적 재생반응에 미치는 영향을 고찰하였다. Zinc ferrite 흡착제가 가장 높은 황화수소 제거능을 나타내었고 혼합한 $Fe_2O_3$ 흡착제는 황화반응 도중 H$_2$S의 생성을 촉진시킴을 알 수 있었다. 또한 황화반응의 결과로 생성되는 금속황화물들이 H$_2$S 열분해의 촉매로 작용하였으며 H$_2$$Fe_2O_3$의 함량이 증가할수록 더 많이 발생하였다. 산화적 재생반응의 결과로부터 ZnS를 제외하고 $Fe_2O_3$를 혼합한 흡착제는 모두 잘 재생됨을 알 수 있었다. 또한 산화적 재생반응 도중 생성될 수 있다고 보고된 zinc sulfate는 생성되지 않았다. 그리고 SO$_2$ 발생 곡선의 형태나 완전재생에 소요되는 시간을 기준으로 판단해 볼 때 $Fe_2O_3$의 혼합량의 변화는 산화적 재생반응에 별다른 영향을 미치지 않음을 알 수 있었다.

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촉매-플라즈마 반응 시스템을 이용한 황화수소의 처리특성 연구 (Characteristics of Hydrogen Sulfide Removal by a Catalyst-assisted Plasma System)

  • 이정근;김혁규;봉춘근;박성진;이명화;황의현;김종호
    • 한국대기환경학회지
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    • 제27권4호
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    • pp.379-386
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    • 2011
  • Catalyst-assisted plasma system with a DBD (Dielectric Barrier Discharge) reactor was used to remove hydrogen sulfide, which is one of the odorous species in this study. The ${\gamma}-Al_2O_3$ and ${\beta}$-Zeolite catalysts impregnated by Ag, Cu and Mn species were employed as catalysts and their $H_2S$ removal characteristics under plasma irradiation were investigated. From the experimental study, we found that the $H_2S$ removal efficiency increases with decreasing space velocity in the system and increasing specific input energy. Furthermore, ${\beta}$-Zeolite catalysts are efficient to remove $H_2S$ than ${\gamma}-Al_2O_3$ catalysts. Especially, the catalysts impregnated by Ag have higher removal efficiency than other catalysts (Cu, Mn).

Biomedia를 충전한 Biofilter에서 H2S와 NH3 혼합악취의 제거 (Removal of Mixed Gases of H2S and NH3 by the Biofilter Packed with Biomedia)

  • 임정수;조욱상;이은영
    • 청정기술
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    • 제12권3호
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    • pp.165-170
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    • 2006
  • Polyurethane, PVA(polyvinyl alcohol)와 지렁이 분변토로 제작한 biomedia를 충진한 바이오필터(biofilter)를 이용하여 $H_2S$$NH_3$의 혼합 악취를 제거하였다. $NH_3$ 농도를 50 ppmv로 고정시킨 후, $H_2S$의 농도는 1~489 ppmv까지 증가시키며 제거효율을 살펴보았다. 또한 $NH_3$의 농도를 점진적으로 증가시켜 80, 100, 200, 300, 400, 500 ppmv 으로 설정하여 각각의 $NH_3$농도가 고정된 조건에서는 $H_2S$를 점차적으로 농도를 증가시켜주며 $NH_3$$H_2S$ 가스의 제거효율을 알아보았다. 혼합 악취가 공급되는 조건에서 $NH_3$의 유입 부하량은 입구농도가 50~300 ppmv 까지는 부하량 $11.14g\;N{\cdot}m^{-3}{\cdot}h^{-1}$이 증가함에 따라 제거용량도 비례하여 증가하였다. 입구농도가 300 ppmv 이상으로 증가함에 따라 유입 부하량은 증가하는 반면, 제거효율과 제거용량은 감소되는 것을 볼 수 있었다. 복합악취가 공급되는 조건에서 $H_2S$ 최대 부하량은 $40.27g\;S{\cdot}m^{-3}{\cdot}h^{-1}$이하이며, $NH_3$ 부하량이 $15.25g\;N{\cdot}m^{-3}{\cdot}h^{-1}$ 이하인 조건에서는 $NH_3$의 공급에 의해 $H_2S$의 제거효율은 큰 영향을 받지 않는 것으로 나타났다.

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Degradation of toxic azo dye (AO7) using Fenton's process

  • Sharma, Ashish;Verma, Manisha;Haritash, A.K.
    • Advances in environmental research
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    • 제5권3호
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    • pp.189-200
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    • 2016
  • This study aimed at advanced oxidation of hetero tri-functional reactive dye Acid orange 7 using photo-Fenton conditions in a lab-scale experiment. Decolourisation of Acid Orange 7 dye by Fenton's process was dependent on concentration of Hydrogen peroxide, Ferrous sulphate, pH, and contact time. A $2^3$ factorial design was used to evaluate the effects of these key factors: pH, Fe(II), and $H_2O_2$ concentration, for a dye concentration of 50 mg/L with COD of 340 mg/L at pH 3.0. The response function was removal of colour under optimised conditions; pH 3.0, [Fe(II)] 40.83 mg/L, [$H_2O_2$] 4.97 mmol/L; 13.6 min. of treatment resulting in 100% colour removal. The final COD of treated wastewater was nil suggesting that AOP is a potentially useful process of color removal and dye degradation/mineralisation of effluent having AO7. Minimum contact time for complete decolourisation was at 5 mmol/l $H_2O_2$ concentration. Increase in $FeSO_4$ (mg/l) concentration resulted in decrease of time for complete decolourisation. Box-Behnken Design was used to optimize the process variables. Maximum and minimum levels of pH (3-5), $H_2O_2$ (4-6 mmol/l), $FeSO_4$ (30-46 mg/l) and contact time (5-15 minutes) were used. The statistical analysis revealed a value of 0.88 for coefficient of regression ($R^2$) indicating a good fit of model. Calculated F-value was found higher than the tabulated value confirming to significance of the model. Based on student's t-test, Ferrous sulphate, pH, and contact time have a positive effect on the percent decolourisation of Acid Orange 7.

Cholesterol Removal from Lard with Crosslinked ${\beta}$-Cyclodextrin

  • Kim, S.H.;Kim, H.Y.;Kwak, H.S.
    • Asian-Australasian Journal of Animal Sciences
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    • 제20권9호
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    • pp.1468-1472
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    • 2007
  • The present study was carried out to determine the optimum conditions of different factors (ratio of lard to water, ${\beta}$-CD concentrations, mixing temperature, mixing time and mixing speed) on cholesterol reduction from lard by using crosslinked ${\beta}$-CD. Crosslinked ${\beta}$-CD was prepared with adipic acid. When the lard was treated under different conditions, the range of cholesterol removal was 91.2 to 93.0% with 5% crosslinked ${\beta}$-CD, which was not significantly different among treatments. In a recycling study, cholesterol removal with crosslinked ${\beta}$-CD in the first trial was 92.1%, which was similar to that with new crosslinked ${\beta}$-CD. In up to eight time trials, over 90% of cholesterol removal was found. The present study indicated that the optimum conditions for cholesterol removal using crosslinked ${\beta}$-CD were a 1:3 ratio of lard to water, 5% crosslinked ${\beta}$-CD concentration, $40^{\circ}C$ mixing temperature, 1 h mixing time and 150 rpm mixing speed. In addition, crosslinked ${\beta}$-CD made by adipic acid resulted in an effective recycling efficiency.

Sexual Behaviors, Estrus Detection and Conception of Heifers Synchronized by Progesterone Intravaginal Device(Prid) and Synchromate-B

  • Im, K.S.;Kim, C.K.;Voss, H.J.;Allen, S.;Zheng, X.;Foote, R.H.
    • 한국가축번식학회지
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    • 제9권2호
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    • pp.140-147
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    • 1985
  • Seventy four Holstein heifers were randomly assigned over three trials to PRID-7+PG-6 and Synchromate B-9 regimens to synchronize estrus cycle for embryo transfer. Sexual behaviors; moounting, standing, orientation, chin-resting, sniffing, licking, rubbing and butting, vaginal swelling and mucus discharge were observed between 06-08, 12-14 and 18-20 h on 1st day and 00-02, 06-08, 12-14 and 18-20 h on 2nd day after removal of hormones. Synchromate-B treatment (81.6%) showed higher synchronized estrus rate than PRID treatment (77.8%) during observation period. Standing estrus was observed within 74 h after PG injection in PRID and within 52 h after removal of implant in Synchromate-B. About 68% of heifers in PRID and 74% of heifers in Synchromate-B showed standing estrus between 0-14 h on 2nd day after removal of the hormones. Synchromate-B resulted in a tighter synchrony of standing estrus than PRID. Incidence of average mounting and standing per head during observation period was 22.3 and 16.6 in PRID and 28.1 and 13.6 in Synchromate-B. The PRID showed peak in active mounting at 18-20 h on 1st day, however, the Synchromate-B showed at 0-2 h on 2nd day after removal of hormone. Active standing was shown between 18 h on 1st day to 20h on 2nd day in PRID, however, between 0-14 h on 2nd day after removal of hormone is Synchromate-B. There was slight difference in pattern of active mounting and standing during estrus between PRID and Synchromate-B. Conception rate of synchronized heifers transferred with fresh and frozen embryos by non-surgical and surgical methods was higher in synchromate-B (62.5%) than in PRID (38.5%). Chin-resting showed highest incidence among 6 sexual behavioral components in the both treatments. Synchromate-B showed higher incidence of chin-resting (16.6) than PRID (10.7). Synchromate-B group showed also higher incidence of orientation, sniffing and butting than PRID group. Synchromate-B resulted in more active sexual behaviors than PRID. The pattern of incidence of chin-resting, licking and butting was almost symmetrical in PRID with their peak values at 6-8 h on 2nd day, however in Synchromate-B chin-resting and sniffing was symmetrical with their peak values at 12-14 h on 2nd day after removal of hormone. There was tendency to increase vaginal swelling according to time passage of synchronized estrus in the both treatments. Incidence of mucus discharge in Synchromate-B was slightly higher than in PRID. Twenty to 40% was false negative in conception rate by tall painting before re-estrus day as judged by rectal palpation.

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Evaluation of Effective Process Operation for the Texitile Dyeing Wastewater by Ferrous Solution and Hydrogen Peroxide

  • Lee, Sang Ho;Moon, Hey Jin
    • 한국환경과학회지
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    • 제13권11호
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    • pp.987-991
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    • 2004
  • The purpose of this research is to evaluate the removal efficiencies of COD$\_$Cr/ and color for the dyeing wastewater by the different dosages of ferrous solution and H$_2$O$_2$ in Fenton process. In the case of H$_2$O$_2$ divided dosage for the Fenton's reagent 7:3 of H$_2$O$_2$ was more effective than 3:7 to remove COD$\_$Cr/ and color. The results showed that COD$\_$Cr/ was mainly removed by Fenton coagulation, where the ferric ions are formed in the initial step of Fenton reaction. On the other hand color was removed by Fenton oxidation rather than Fenton coagulation. The removal mechanism of COD$\_$Cr/ and color was mainly coagulation by ferrous ion, ferric ion and Fenton oxidation. The removal efficiencies were dependent on the ferric ion amount at the beginning of the reaction. However, the final removal efficiency of COD$\_$Cr/ and color was in the order of Fenton oxidation, ferric ion coagulation and ferrous ion coagulation. The reason of the highest removal efficiency by Fenton oxidation can be explained by the chain reactions with ferrous solution, ferric ion and hydrogen peroxide.

EFFECT OF INLET LOADING RATE ON THE ELIMINATION OF HYDROGEN SULFIDE AND AMMONIA IN IMMOBILIZED CELL BIOFILTERS

  • Kim, Jung-Hoon;Rene, Eldon R.;Park, Seung-Han;Park, Hung-Suck
    • Environmental Engineering Research
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    • 제11권5호
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    • pp.285-291
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    • 2006
  • Biofiltration is a simple, effective, economically viable and the most widely used gas treatment technique for treating malodors at low concentrations and high flow rates. This paper reports the performance of two lab scale immobilized cell biofilters operated in continuous mode for hydrogen sulfide ($H_2S$) and ammonia ($NH_3$) removal. The removal efficiency (RE, %) and the elimination capacity (EC, $g/m^3{\cdot}hr$) profiles were monitored by subjecting the biofilters to different loading rates of $H_2S$ (0.3 to $8\;g/m^3{\cdot}hr$) and $NH_3$ (0.3 to $4.5\;g/m^3{\cdot}hr$). The removal efficiencies were greater than 99% when inlet loading rate to the biofilters were upto $6\;gH_2S/m^3{\cdot}hr$ and $4\;gNH_3/m^3{\cdot}hr$ respectively. The performance of the biofilters were also ascertained by conducting shock loading studies at a loading rate of $10\;gH_2S/m^3{\cdot}hr$ and $6\;gNH_3/m^3{\cdot}hr$. The results from this study show high removal efficiency, good recuperating potential and stability of the immobilized microbial consortia to transient shock loads.

생물탈취상에 의한 도시폐기물 매립지가스내 악취물질의 처리 (Biofiltration of Odorous Compounds in Municipal Solid Waste Landfill Gases)

  • 남궁완;박준석;황의영;이노섭;인병훈;김정대
    • 한국토양환경학회지
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    • 제4권1호
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    • pp.85-96
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    • 1999
  • 퇴비를 충전물질로 사용한 생물탈취상으로 난지도매립지에서 발생되는 매립지가스 처리시 악취유발물질 및 휘발성 유기화합물의 제거특성과 생물탈취상의 적용가능성을 평가하고자 하였다 본 연구는 난지도매립지 상부에서 실시하였으며 충전물질로는 난지도퇴비화시범시설에서 생산된 퇴비를 사용하였다. 약 15ppmv로 유입된 황화수소는 25cm충전깊이에서도 98%이상 제거되었으며 산소공급중단 후 혐기성가스만 유입시에는 처리효율이 30%로 저하하였다. 평균유입농도 40ppmv에서의 암모니아 제거 효율은 85%정도이었다. BTEX중 톨루엔과 에틸벤젠의 제거효율은 80%로 벤젠과 자일렌보다 높았다. 수분손실은 가스유입구에서 가장 높게 나타났으며 약 30일 운전기간 동안 pH저하에 의한 산성화는 발생하지 않았다.

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